CN206103674U - System for agent of preparation flue gas desulfurization - Google Patents
System for agent of preparation flue gas desulfurization Download PDFInfo
- Publication number
- CN206103674U CN206103674U CN201621015016.0U CN201621015016U CN206103674U CN 206103674 U CN206103674 U CN 206103674U CN 201621015016 U CN201621015016 U CN 201621015016U CN 206103674 U CN206103674 U CN 206103674U
- Authority
- CN
- China
- Prior art keywords
- pump
- flue gas
- muddy water
- high salt
- gas desulfurization
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired - Fee Related
Links
- 230000003009 desulfurizing Effects 0.000 title claims abstract description 25
- UGFAIRIUMAVXCW-UHFFFAOYSA-N carbon monoxide Chemical compound [O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 title claims abstract description 21
- 239000003546 flue gas Substances 0.000 title claims abstract description 21
- 238000006477 desulfuration reaction Methods 0.000 title claims abstract description 19
- 239000003795 chemical substances by application Substances 0.000 title claims abstract description 16
- 238000002360 preparation method Methods 0.000 title abstract 5
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 74
- 239000011780 sodium chloride Substances 0.000 claims abstract description 37
- 150000003839 salts Chemical class 0.000 claims abstract description 35
- 238000005520 cutting process Methods 0.000 claims abstract description 12
- 238000000227 grinding Methods 0.000 claims abstract description 10
- 229910052731 fluorine Inorganic materials 0.000 claims description 14
- 239000011737 fluorine Substances 0.000 claims description 14
- YCKRFDGAMUMZLT-UHFFFAOYSA-N fluorine atom Chemical compound [F] YCKRFDGAMUMZLT-UHFFFAOYSA-N 0.000 claims description 14
- 229920000647 polyepoxide Polymers 0.000 claims description 12
- 239000011248 coating agent Substances 0.000 claims description 11
- 238000000576 coating method Methods 0.000 claims description 11
- 239000003822 epoxy resin Substances 0.000 claims description 11
- 239000002002 slurry Substances 0.000 claims description 7
- 239000007921 spray Substances 0.000 claims description 4
- 238000004891 communication Methods 0.000 claims description 3
- 230000000694 effects Effects 0.000 abstract description 8
- 239000010842 industrial wastewater Substances 0.000 abstract description 8
- 238000004140 cleaning Methods 0.000 abstract description 6
- 239000007788 liquid Substances 0.000 abstract description 6
- 238000005516 engineering process Methods 0.000 abstract description 5
- 239000003344 environmental pollutant Substances 0.000 abstract description 3
- 231100000719 pollutant Toxicity 0.000 abstract description 3
- 238000005507 spraying Methods 0.000 abstract 1
- 238000000034 method Methods 0.000 description 10
- 230000005684 electric field Effects 0.000 description 9
- 239000002351 wastewater Substances 0.000 description 9
- 239000000460 chlorine Substances 0.000 description 8
- ODINCKMPIJJUCX-UHFFFAOYSA-N calcium monoxide Chemical compound [Ca]=O ODINCKMPIJJUCX-UHFFFAOYSA-N 0.000 description 5
- XEEYBQQBJWHFJM-UHFFFAOYSA-N iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 description 5
- BHPQYMZQTOCNFJ-UHFFFAOYSA-N calcium cation Chemical compound [Ca+2] BHPQYMZQTOCNFJ-UHFFFAOYSA-N 0.000 description 4
- 229910001424 calcium ion Inorganic materials 0.000 description 4
- 229910052801 chlorine Inorganic materials 0.000 description 4
- ZAMOUSCENKQFHK-UHFFFAOYSA-N chlorine atom Chemical compound [Cl] ZAMOUSCENKQFHK-UHFFFAOYSA-N 0.000 description 4
- 239000012267 brine Substances 0.000 description 3
- 238000005039 chemical industry Methods 0.000 description 3
- MHAJPDPJQMAIIY-UHFFFAOYSA-N hydrogen peroxide Chemical compound OO MHAJPDPJQMAIIY-UHFFFAOYSA-N 0.000 description 3
- 150000002500 ions Chemical class 0.000 description 3
- 229910001425 magnesium ion Inorganic materials 0.000 description 3
- MYMOFIZGZYHOMD-UHFFFAOYSA-N oxygen Chemical compound O=O MYMOFIZGZYHOMD-UHFFFAOYSA-N 0.000 description 3
- 239000002699 waste material Substances 0.000 description 3
- 239000004593 Epoxy Substances 0.000 description 2
- 235000019738 Limestone Nutrition 0.000 description 2
- 229910000831 Steel Inorganic materials 0.000 description 2
- 230000002745 absorbent Effects 0.000 description 2
- 239000002250 absorbent Substances 0.000 description 2
- 238000010521 absorption reaction Methods 0.000 description 2
- 239000011575 calcium Substances 0.000 description 2
- VTYYLEPIZMXCLO-UHFFFAOYSA-L calcium carbonate Chemical compound [Ca+2].[O-]C([O-])=O VTYYLEPIZMXCLO-UHFFFAOYSA-L 0.000 description 2
- 239000000292 calcium oxide Substances 0.000 description 2
- 235000012255 calcium oxide Nutrition 0.000 description 2
- OKTJSMMVPCPJKN-UHFFFAOYSA-N carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 2
- 239000003245 coal Substances 0.000 description 2
- 125000003700 epoxy group Chemical group 0.000 description 2
- 238000001704 evaporation Methods 0.000 description 2
- 238000010304 firing Methods 0.000 description 2
- 229910052742 iron Inorganic materials 0.000 description 2
- 239000006028 limestone Substances 0.000 description 2
- 239000001301 oxygen Substances 0.000 description 2
- 229910052760 oxygen Inorganic materials 0.000 description 2
- 238000010248 power generation Methods 0.000 description 2
- 238000000746 purification Methods 0.000 description 2
- 239000010959 steel Substances 0.000 description 2
- RAHZWNYVWXNFOC-UHFFFAOYSA-N sulphur dioxide Chemical compound O=S=O RAHZWNYVWXNFOC-UHFFFAOYSA-N 0.000 description 2
- 150000003568 thioethers Chemical class 0.000 description 2
- BVKZGUZCCUSVTD-UHFFFAOYSA-M Bicarbonate Chemical compound OC([O-])=O BVKZGUZCCUSVTD-UHFFFAOYSA-M 0.000 description 1
- 229910001369 Brass Inorganic materials 0.000 description 1
- 229960005069 Calcium Drugs 0.000 description 1
- AXCZMVOFGPJBDE-UHFFFAOYSA-L Calcium hydroxide Chemical compound [OH-].[OH-].[Ca+2] AXCZMVOFGPJBDE-UHFFFAOYSA-L 0.000 description 1
- GBAOBIBJACZTNA-UHFFFAOYSA-L Calcium sulfite Chemical compound [Ca+2].[O-]S([O-])=O GBAOBIBJACZTNA-UHFFFAOYSA-L 0.000 description 1
- 241000276438 Gadus morhua Species 0.000 description 1
- 210000002381 Plasma Anatomy 0.000 description 1
- CVTZKFWZDBJAHE-UHFFFAOYSA-N [N].N Chemical compound [N].N CVTZKFWZDBJAHE-UHFFFAOYSA-N 0.000 description 1
- 239000010951 brass Substances 0.000 description 1
- OYPRJOBELJOOCE-UHFFFAOYSA-N calcium Chemical compound [Ca] OYPRJOBELJOOCE-UHFFFAOYSA-N 0.000 description 1
- 229910052791 calcium Inorganic materials 0.000 description 1
- 229910000019 calcium carbonate Inorganic materials 0.000 description 1
- 239000000920 calcium hydroxide Substances 0.000 description 1
- 235000011116 calcium hydroxide Nutrition 0.000 description 1
- 229910001861 calcium hydroxide Inorganic materials 0.000 description 1
- 235000010261 calcium sulphite Nutrition 0.000 description 1
- VMLAJPONBZSGBD-UHFFFAOYSA-L calcium;hydrogen carbonate;hydroxide Chemical compound [OH-].[Ca+2].OC([O-])=O VMLAJPONBZSGBD-UHFFFAOYSA-L 0.000 description 1
- FBEDQOZZWWECAJ-UHFFFAOYSA-M calcium;magnesium;hydroxide Chemical compound [OH-].[Mg+2].[Ca+2] FBEDQOZZWWECAJ-UHFFFAOYSA-M 0.000 description 1
- 238000006243 chemical reaction Methods 0.000 description 1
- VEXZGXHMUGYJMC-UHFFFAOYSA-M chloride anion Chemical compound [Cl-] VEXZGXHMUGYJMC-UHFFFAOYSA-M 0.000 description 1
- 235000019504 cigarettes Nutrition 0.000 description 1
- 235000019516 cod Nutrition 0.000 description 1
- 239000000084 colloidal system Substances 0.000 description 1
- 239000006071 cream Substances 0.000 description 1
- 238000010612 desalination reaction Methods 0.000 description 1
- 229910001882 dioxygen Inorganic materials 0.000 description 1
- 230000005685 electric field effect Effects 0.000 description 1
- 230000005611 electricity Effects 0.000 description 1
- 238000010894 electron beam technology Methods 0.000 description 1
- 238000005265 energy consumption Methods 0.000 description 1
- 239000007789 gas Substances 0.000 description 1
- 239000008187 granular material Substances 0.000 description 1
- 239000010440 gypsum Substances 0.000 description 1
- 229910052602 gypsum Inorganic materials 0.000 description 1
- XLYOFNOQVPJJNP-ZSJDYOACSA-N heavy water Substances [2H]O[2H] XLYOFNOQVPJJNP-ZSJDYOACSA-N 0.000 description 1
- 125000002887 hydroxy group Chemical group [H]O* 0.000 description 1
- 239000012535 impurity Substances 0.000 description 1
- 238000009776 industrial production Methods 0.000 description 1
- 244000144972 livestock Species 0.000 description 1
- FYYHWMGAXLPEAU-UHFFFAOYSA-N magnesium Chemical compound [Mg] FYYHWMGAXLPEAU-UHFFFAOYSA-N 0.000 description 1
- 239000011777 magnesium Substances 0.000 description 1
- 229910052749 magnesium Inorganic materials 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 239000012528 membrane Substances 0.000 description 1
- 230000005012 migration Effects 0.000 description 1
- 230000003647 oxidation Effects 0.000 description 1
- 238000007254 oxidation reaction Methods 0.000 description 1
- CBENFWSGALASAD-UHFFFAOYSA-N ozone Chemical compound [O-][O+]=O CBENFWSGALASAD-UHFFFAOYSA-N 0.000 description 1
- 239000002245 particle Substances 0.000 description 1
- 238000001556 precipitation Methods 0.000 description 1
- 239000010865 sewage Substances 0.000 description 1
- 239000000779 smoke Substances 0.000 description 1
- 239000007787 solid Substances 0.000 description 1
- 239000000243 solution Substances 0.000 description 1
- 239000004575 stone Substances 0.000 description 1
- 238000003860 storage Methods 0.000 description 1
- NINIDFKCEFEMDL-UHFFFAOYSA-N sulfur Chemical compound [S] NINIDFKCEFEMDL-UHFFFAOYSA-N 0.000 description 1
- 229910052717 sulfur Inorganic materials 0.000 description 1
- 239000011593 sulfur Substances 0.000 description 1
- 238000005429 turbidity Methods 0.000 description 1
- 238000005406 washing Methods 0.000 description 1
- 239000003403 water pollutant Substances 0.000 description 1
Abstract
The utility model provides a system for agent of preparation flue gas desulfurization, relates to the industrial pollutant reutilization technology field for utilize the agent of industrial waste water preparation flue gas desulfurization. A system for agent of preparation flue gas desulfurization, characterized by, electromagnetism dirt pocket set up in high salt high muddy water pond, inlet tube and outlet pipe respectively and the high muddy water pond of high salt intercommunication, the outlet pipe with the clean water basin intercommunication, the top in the high muddy water pond of high salt is provided with the guide rail, the lifting mechanism sliding connection be in on the guide rail, collect dirty trench in the below of guide rail, the collection dirty groove with cutting grinding pump's import intercommunication, the cutting grinding pump the export with dirt dressing trough intercommunication, the import of first thick liquid pump with dirt dressing trough intercommunication, first thick liquid delivery side of pump with thick liquid groove intercommunication, second thick liquid delivery side of pump is connected with spraying system in the desulfurizing tower. The beneficial effects are that, can utilize industrial waste water preparation desulfurizer.
Description
Technical field
This utility model is related to industrial pollutants reutilization technology field, and specifically one kind prepares flue gas desulfurization agent
System.
Background technology
The industrial wastewater produced in the industrial undertaking such as chemical industry, iron and steel, thermal power generation production process can be divided into according to salinity
Two classes:One is organic wastewater, is mainly derived from coal gasifying process waste water, process units waste water and sanitary sewage etc., is characterized in
Salinity is low, pollutant are based on COD and ammonia nitrogen；Two is brine waste, after being mainly derived from circulation concentration and evaporation
Sewer, DW system demineralized water system draining, boiler blowdown water, reclaiming system concentrated water etc., are characterized in that suspended solid and salinity are high, contain
The total salinity (TDS) of salt waste water is generally in 500～5000m g/L.
With the increasingly raising of environmental requirement, industrial fresh water consumption indicators and water pollutant discharge standard are increasingly strict,
Brine waste reuse is unprecedentedly paid attention to.Brine waste reuse at present is generally using membrance concentration or hot concentration technique by waste water
Impurity is concentrated, and clear water is back to circulation, and dope (high-salt wastewater) is separately processed.Membrance concentration technology has influent quality will
Ask higher, not high, the clear water response rate that is susceptible to dirty stifled, cycles of concentration it is low (typically 60% to 80%, efficient reverse osmosiss
(HERO) can reach 90%), the shortcomings of produce certain amount intractability bigger high-salt wastewater；Heat concentration mainly has multiple-effect to steam
Send out, mechanical compress evaporation, the mode such as Membrane Materials, there is huge equipment, high energy consumption, generation certain amount intractability more in the technology
Big haline water (the clear water response rate is typically 90% or so).Saliferous industrial wastewater " zero-emission " although basic feasible solution in theory,
But there is many difficult points in actual industrial production practice, waste water integrated with the stability of main process, unit for treating water technique
Reuse scheduling etc. is closely related.At present, for coal chemical industry, China not yet has an enterprise really to realize waste water " zero-emission
Put ".
On the other hand, coal-burning boiler with enterprises such as the increasingly summary of environmental requirement, chemical industry, iron and steel, thermal power generation, burning
Sulfide content is required increasingly strictly in knot machine, tubular heater smoke evacuation tail gas, is that this most enterprise is additionally arranged flue gas
Desulfurization equipment.The most commonly used wet desulfurization of flue gas by limestone-gypsum method technique of domestic application is with limestone, quick lime or disappears
The thick liquid of Calx is the sulfur dioxide that absorbent is absorbed in flue gas, and the calcium sulfite of generation is obtained stone Jing after air oxidation
Cream.The method needs a number of limestone of regular replenishment, quick lime or slaked lime as the absorbent of sulfide in flue gas.
Utility model content
The purpose of this utility model is to provide a kind of system for preparing flue gas desulfurization agent, for using industrial wastewater system
Standby flue gas desulfurization agent.
This utility model solves the technical scheme that its technical problem adopted：It is a kind of prepare flue gas desulfurization agent be
System, including the high muddy water pond of high salt, electromagnetism dirt pocket, lifter, scale collecting slot, cutting and grinding pump, dirty stock tank, the first serosity pump, slurry
Liquid bath, the second serosity pump and clear water reserviors, the electromagnetism dirt pocket is arranged in the high muddy water pond of the high salt, the high muddy water of the high salt
Pond includes water inlet pipe and outlet pipe, and, near the lower end of the high muddy water pond of the high salt, the outlet pipe is near described for the water inlet pipe
The upper end of the high muddy water pond of high salt, the water inlet pipe and outlet pipe are connected respectively with the high muddy water pond of the high salt, the outlet pipe with
Clear water reserviors connection, above the high muddy water pond of the high salt guide rail is provided with, and the lifter is slidably connected at the guide rail
On；
The scale collecting slot is located at the lower section of the guide rail, the inlet communication of the scale collecting slot and the cutting and grinding pump, institute
The outlet for stating cutting and grinding pump is connected with the dirty stock tank, and the import of the first serosity pump is connected with the dirty stock tank, described
The outlet of the first serosity pump is connected with the slurry tank, and outlet and the spray system in desulfurizing tower of the second serosity pump connect
Connect.
Further, further, the quantity of the reservoir chamber is three.
Further, the electromagnetism dirt pocket includes fluorine-containing epoxy resin coating, and fluorine-containing epoxy resin coating is coated on institute
State the outer surface of electromagnetism dirt pocket.
Further, the thickness of the fluorine-containing epoxy resin coating is between 6nm～10nm, including 6nm and 10nm.
The beneficial effects of the utility model are：
1st, a kind of system for preparing flue gas desulfurization agent that this utility model is provided, it is possible to use industrial wastewater is cigarette
Desulfurization duty for desulfurizing agent, with the characteristics of environmental protection and energy saving.
2nd, the high muddy water pond of the high salt includes some reservoir chambers, and each reservoir chamber is sequentially connected in series, respectively sets in each reservoir chamber
There is an electromagnetism dirt pocket, the water inlet pipe connect with the reservoir chamber positioned at stem, the outlet pipe and the water storage positioned at afterbody
Room connects.This not only can ensure that industrial wastewater can more thoroughly be processed, it is ensured that the clear water clean-up performance after process is carried
It is high.And can ensure that and be placed with electromagnetic cleaner all the time in the high muddy water pond of high salt, it is ensured that the continuous firing of system.
3rd, the quantity of the reservoir chamber is three.This makes staff be easy to safeguard system, and in turn ensure that
The continuous firing ability of system.
4th, the electromagnetism dirt pocket includes fluorine-containing epoxy resin coating, and fluorine-containing epoxy resin coating is coated on the electromagnetism collection
The outer surface of dirty device.Jing experimental demonstrations, dirty is not easy to stick to the surface of fluorine-containing epoxy layer, institute in the case where external force is not received
Can ensure that dirty naturally can come off from electromagnetism dirt pocket surface after electromagnetism dirt pocket power-off with fluorine-containing epoxy layer, from
And improve the automatical cleaning ability of electromagnetism dirt pocket.
5th, the thickness of the fluorine-containing epoxy resin coating is between 6nm～10nm, including 6nm and 10nm.This thickness model
Enclose and both can ensure that electromagnetism dirt pocket, in the energized state to the absorption affinity of dirty, can ensure that electromagnetism dirt pocket in power-off feelings again
Automatical cleaning ability under condition.
Description of the drawings
Fig. 1 is structural representation of the present utility model；
In figure：The high muddy water pond of 1 high salt, 11 electromagnetism dirt pockets, 12 water inlet pipes, 13 outlet pipes, 14 clear water reserviors, 15 reservoir chambers, 2
Lifter, 21 guide rails, 3 scale collecting slots, 4 cutting and grinding pumps, 5 dirty stock tanks, 6 first serosity pumps, 7 slurry tanks, 8 second serosity pumps, 9 take off
Sulfur tower, 91 air-introduced machines.
Specific embodiment
It is new below in conjunction with this practicality to make purpose, technical scheme and the advantage of this utility model embodiment clearer
Accompanying drawing in type embodiment, is clearly and completely described, it is clear that retouched to the technical scheme in this utility model embodiment
The embodiment stated is a part of embodiment of the present utility model, rather than the embodiment of whole.Based on the reality in this utility model
Apply example, the every other embodiment that those of ordinary skill in the art are obtained on the premise of creative work is not made, all
Belong to the scope of this utility model protection.
As shown in figure 1, electromagnetism dirt pocket 11 is arranged in the high muddy water pond 1 of the high salt, electromagnetism dirt pocket 11 includes fluorine-containing
Epoxy coating, fluorine-containing epoxy resin coating is coated on 11 outer surfaces of electromagnetism dirt pocket.The thickness of fluorine-containing epoxy resin coating
Degree is between 6nm～10nm, including 6nm and 10nm.The high muddy water pond 1 of high salt includes water inlet pipe 12 and outlet pipe 13, water inlet pipe 12
Near the lower end in high turbid 1 pond of high salt, outlet pipe 13 is near the upper end of the high muddy water pond of the high salt, water inlet pipe 12 and outlet pipe 13
Connect with the high muddy water pond 1 of high salt respectively, outlet pipe 13 is connected with clear water reserviors 14, the high muddy water pond of high salt includes some reservoir chambers
15, each reservoir chamber is sequentially connected in series, and electromagnetism dirt pocket is respectively provided with each reservoir chamber, and water inlet pipe 12 connects with the reservoir chamber for being located at stem
Logical, outlet pipe 13 is connected with the reservoir chamber positioned at afterbody.
The top of the high muddy water pond 1 of high salt is provided with guide rail 21, and lifter 2 is slidably connected on guide rail 21, and scale collecting slot 3 is located at
The inlet communication of the lower section of guide rail 21, scale collecting slot 3 and cutting and grinding pump 4, the outlet of cutting and grinding pump 4 is connected with dirty stock tank 5, the
The import of one serosity pump 6 is connected with dirty stock tank 5, and the outlet of the first serosity pump 6 is connected with slurry tank 7, the outlet of the second serosity pump 8
It is connected with the spray system in desulfurizing tower, spray system is a kind of prior art.
As shown in figure 1, this utility model is when work, high salt high-turbidity industrial wastewater is entered simultaneously by water inlet pipe 12
Centralized collection is in the high muddy water pond 1 of high salt；When the high muddy water of high salt flows through electromagnetism dirt pocket 11, powered Ca2+, Mg2+Plasma,
Group granule forms new active zone electroprecipitation and accumulates in electricity under electrochemical action and electric microfield effect with carbanion in water
The surface of magnetic dirt pocket 11；The high muddy water of high salt flowing full successively in the reservoir chamber 15 of three arranged in series；Periodically pass through lifter 2
Electromagnetism dirt pocket 11 is taken out into cleaning dirty, is cleared up one by one in units of the reservoir chamber of arranged in series during cleaning dirty, realize system
The continuous operation of system.Electromagnetism dirt pocket is transferred to by the top of scale collecting slot 3 by lifter 2, the part electromagnetism dirt pocket power-off is given,
Accumulate in the dirty on electromagnetism dirt pocket to depart from in scale collecting slot 3 from surface automatically；With soft brass scraper by electromagnetism dirt pocket
Surface is again put back to electromagnetism dirt pocket in the high muddy water pond of high salt, so by lifter 2 after removing totally without departing from clean dirty
Afterwards electromagnetism dirt pocket is powered and works on.Then water flowing full after process to clear water carries out follow-up place again into clear water reserviors 14
Reason.The dirty that scale collecting slot 3 is sent is crushed to after diameter 0.5mm to 1mm and is sent in dirty stock tank 5 by cutting and crushing pump 4, then again by
First serosity pump 6 is delivered in slurry tank 7 and stores, then is delivered to the top of flue gas desulfurization tower 9 by the second serosity pump 8 and is sprayed
Spill, the flue gas that the conveying of purification and washing air-introduced machine 91 comes in desulfurizing tower 9.
Electromagnetism dirt pocket operation principle：During work, 11 points of electromagnetism dirt pocket is A, B electric field functional areas, and A electric fields functional areas exist
Calcium, the insoluble micel of magnesium high activity are formed under the effect of high-frequency impulse electron beam stream and is formed containing molecule structure with other ions in water
The macromolecular mass of frame, while under electric field force constraint, macromolecular mass " sandwiches, wraps up in and take " other ions and together analysing on dirt pocket surface
Go out.In this course, possess the new active powered micel of Calcium Carbonate and magnesium hydroxide of huge specific surface area also in a large number absorption,
Float, colloid etc., make water quality be purified in " net is caught " water.
In B electric fields functional areas, due to the effect of multi-stage high-frequency pulse electric microfield, electric field intensity is strengthened, and makes water intermediate ion
The rapid migration from B electric fields functional areas adds to A electric fields functional areas, processing procedure is constantly carried out, calcium ions and magnesium ions in water and its
He is removed salt, reaches the target of recirculated water hard-off and desalination after-purification reuse.
Following reaction is produced in processing procedure：
In negative electric field A functional areas charged particles under high-frequency electric field effect, towards the electrode movement electrically contrary with it, claim
For electro-adsorption effect.Into the Fe of internal electric field3+, Ca2+, Mg2+Form precipitation to remove, react as follows：
2H2O(l)+2e→2OH-(aq)+2H
HCO3 -(aq)+OH-(aq)→CO3 2-(aq)+H20(l)
Calcium ion is likely to form Ca (OH)2(dirt), CaCO3(dirt)
In positive electric field A functional areas, the chloride ion of a part is also changed into free chlorine by electric current, while generation drop ozone,
Oxygen-derived free radicals, hydroxyl free radical and dioxygen are water base.This series product provides effect of killing livestock, with reference to Ampere currents and local
High and low (anode) pH regions：
Free chlorine：Cl-- e → Cl (free chlorine)
Hydrogen peroxide：2H2O-2e→H2O2+2H+
Oxygen-derived free radicals：H2O-2e→O+2H+
Free chlorine：Cl+Cl→Cl2↑。
Claims (5)
1. a kind of system for preparing flue gas desulfurization agent, is characterized in that, including the high muddy water pond of high salt, electromagnetism dirt pocket, lifter,
Scale collecting slot, cutting and grinding pump, dirty stock tank, the first serosity pump, slurry tank, the second serosity pump and clear water reserviors, the electromagnetism dirt pocket
In being arranged on the high muddy water pond of the high salt, the high muddy water pond of the high salt includes water inlet pipe and outlet pipe, and the water inlet pipe is near institute
The lower end of the high muddy water pond of high salt is stated, the outlet pipe is near the upper end of the high muddy water pond of the high salt, the water inlet pipe and outlet pipe
Connect with the high muddy water pond of the high salt respectively, the outlet pipe is connected with the clear water reserviors, the top of the high muddy water pond of the high salt
Guide rail is provided with, the lifter is slidably connected on the guide rail；
The scale collecting slot is located at the lower section of the guide rail, and the inlet communication of the scale collecting slot and the cutting and grinding pump is described to cut
The outlet for cutting macerator pump is connected with the dirty stock tank, and the import of the first serosity pump is connected with the dirty stock tank, and described first
The outlet of serosity pump is connected with the slurry tank, and the outlet of the second serosity pump is connected with the spray system in desulfurizing tower.
2. a kind of system for preparing flue gas desulfurization agent according to claim 1, is characterized in that, the high muddy water pond of the high salt
Including some reservoir chambers, each reservoir chamber is sequentially connected in series, and the electromagnetism dirt pocket, the water inlet pipe are respectively provided with each reservoir chamber
Connect with the reservoir chamber positioned at stem, the outlet pipe is connected with the reservoir chamber positioned at afterbody.
3. a kind of system for preparing flue gas desulfurization agent according to claim 2, is characterized in that, the quantity of the reservoir chamber
For three.
4. a kind of system for preparing flue gas desulfurization agent according to claim 1, is characterized in that, the electromagnetism dirt pocket bag
Fluorine-containing epoxy resin coating is included, fluorine-containing epoxy resin coating is coated on the outer surface of the electromagnetism dirt pocket.
5. a kind of system for preparing flue gas desulfurization agent according to claim 4, is characterized in that, the fluorine-containing epoxy resin
The thickness of coating is between 6nm～10nm, including 6nm and 10nm.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201621015016.0U CN206103674U (en) | 2016-08-31 | 2016-08-31 | System for agent of preparation flue gas desulfurization |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201621015016.0U CN206103674U (en) | 2016-08-31 | 2016-08-31 | System for agent of preparation flue gas desulfurization |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN206103674U true CN206103674U (en) | 2017-04-19 |
Family
ID=58516198
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201621015016.0U Expired - Fee Related CN206103674U (en) | 2016-08-31 | 2016-08-31 | System for agent of preparation flue gas desulfurization |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN206103674U (en) |
-
2016
- 2016-08-31 CN CN201621015016.0U patent/CN206103674U/en not_active Expired - Fee Related
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